Page 322 - Reservoir Formation Damage
P. 322

302    Reservoir Formation Damage

                  The  net  mass rate  of deposition  of  small  particles  within  the  filter  cake
               is  given  by:


                            C P21  -                                    (12-136)
                  Rp2s = k d£ t
               which  is  similar  to  Eq.  33  of  Corapcioglu  and  Abboud  (1990),  but  the
               deposition  and  the  mobilization  terms  are  more  consistently  expressed.
                  The rate  expressions  given  by  Eqs.  12-134 through  136 for the  deposi-
               tion  of  the  total  (fine  plus  large)  and  fine  particles  of  the  slurry  over  the
               progressing  cake  surface  and  the  retention  of  the  fine  particles  of  the
               flowing  suspension  within the  cake  matrix  can  be  expressed  in  terms  of
               the  volumetric  rates,  respectively,  as  (Civan,  1999b):




                           1-6 pi  slurry
                                                                        (12-137)







                         d2
                            1-e Pi  Jslurry
                                                                        (12-138)





                           -p2l                                         (12-139)

               In  Eqs.  12-10  through  12, the  slurry  shear-stress,  i s, acting  over  the
               progressing  cake  surface  is  estimated  using  the  Rabinowitsch-Mooney
               equation  (Metzner  and  Reed,  1955).  This  equation  can  be  expressed  for
               linear  and  radial  flow  cases,  respectively,  as  follows:

                  T  =*'(8vV                                            (12-140)

                                                                        (12-141)

                                                        2
               where  k r  and  n  are the consistency  (dyne/cm /s"')  and flow (dimension-
               less)  indices,  which  are  equal  to  the  fluid  viscosity,  jo,  and  unit  for
               Newtonian  fluids,  respectively,  and  v  is  the  tangential  velocity  of  the
               slurry  over the filter  cake  surface.  For static filtration,  v = 0  and  therefore
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